Hybrid model for discharge profile prediction of battery electrode materials using quantum simulations

ABSTRACT

Methods and systems for predicting lithium battery properties are presented. In one embodiment, a method includes an operation for creating an equivalent circuit of a battery cell, where the equivalent circuit includes a cathode equivalent circuit and a remainder equivalent circuit. Further, parameters for the cathode equivalent circuit are calculated using Quantum Mechanical (QM) simulation. Also included in the method are operations for obtaining parameters for the remainder equivalent circuit via experimentation, and for calculating the lithium battery properties using the equivalent circuit.

CROSS REFERENCE TO RELATED APPLICATIONS

This application is related to U.S. patent application Ser. No.12/334,170 filed Dec. 12, 2008, and entitled “FAST AND HIGH-THROUGHPUTSEARCH ENGINE FOR MATERIALS FOR LITHIUM-ION BATTERIES USING QUANTUMSIMULATIONS;” U.S. patent application Ser. No. 12/953,080 filed on thesame day as the instant application and entitled “SIMULATED X-RAYDIFFRACTION SPECTRA FOR ANALYSIS OF CRYSTALLINE MATERIALS;” U.S. patentapplication Ser. No. 12/953,068 filed on the same day as the instantapplication and entitled “LI-ION BATTERY CAPACITY AND VOLTAGE PREDICTIONUSING QUANTUM SIMULATIONS;” and U.S. patent application Ser. No.12/953,048 filed on the same day as the instant application and entitled“QUANTUM-SIMULATIONS DATABASE AND DESIGN ENGINE FOR DEVELOPMENT OFLITHIUM BATTERIES”, all of which are incorporated herein by referencefor all purposes.

BACKGROUND 1. Field of the Invention

The invention relates to the development of Li-ion batteries, and morespecifically, to the use of quantum simulations and modular analysis ofcomposite solid solution cathode and alloyed anode materials structuresfor rapid development of Li-ion batteries.

2. Background of the Invention

Advanced batteries substantially impact the areas of energy storage,energy efficiency, hybrid and plug-in electric vehicles, power tools,laptops, cell phones and many other mobile electronic and entertainmentdevices. Rechargeable lithium-ion batteries offer the highest energydensity of any battery technology and, therefore, are an attractivelong-term technology that now sustains a billion-dollar business. At thematerials level, over the last 30 years the major improvement in theperformance of lithium batteries has been achieved through the discoveryof new lithium cathode materials. LiTiS₂ was the first commercializedcathode material for lithium batteries in the 1970s. LiCoO₂ is currentlythe most active cathode material used in lithium-ion batteries since itsdiscovery in the early 1990s.

However, the safety and high cost of cobalt significantly limits itsapplication to the emerging high capacity and high power batterymarkets. Additionally, the low charge and discharge rate capability is awell-known problem of lithium-ion batteries. Recent efforts in bothindustrial and academic communities to overcome these limitations havebeen focused on compositional modification of LiCoO₂, mainly by infusionwith other transition metal elements, or new architectures for advancedcomposite materials for cathodes.

There has been an interest in the development of an advanced anode usingalloyed materials since commercialization of the graphite anodeaccompanying the LiCoO₂ cathode in the 1990s. Alloyed materials for anadvanced anode and composite materials for an advanced cathode are themainstream approach for next generation Li-ion battery technology. Bothhave the same nature of disorder, in contrast to the well-definedcrystalline structures of LiCoO₂ and graphite.

Searching for new materials by empirical experimental efforts istime-consuming and expensive. Significant efforts are currentlyunderway, mainly in the academic community and Department of Energylaboratories to use quantum simulations (QS) on high performancecomputers to accelerate the search for new and better materials for thebattery industry. Quantum simulations, based on the first-principlesdensity functional theory (DFT) or its equivalent, provide reliablecomputer simulations to predict on atomic-scale the properties ofcurrently known battery materials for cathodes, anodes and electrolytes.The accuracy of the QS-based predictions of materials properties hasbeen proven in a broad range of applications (e.g., semiconductors andpharmaceuticals.)

QS-based first principle DFT methods provide reliable information aboutthe materials structures and the energy associated with makingstructural, electronic, and ionic changes in the materials. The typicalQS methods, however, are time consuming, CPU intensive, and do not scalewell with the size of the system simulated using QS. Few selected casesof Li-ion battery electrode materials in the layer oxide, spinel, andolivine class have been investigated using DFT-based QS (QS-DFT). Thetypical QS-DFT methods for thousands of compositional variations in thelayer oxide, spinel, olivine, and their composites are not feasible withthe current technology.

SUMMARY

Embodiments of the present invention provide methods and systems forpredicting lithium battery properties. It should be appreciated that thepresent invention can be implemented in numerous ways, such as aprocess, an apparatus, a system, a device or a method on a computerreadable medium. Several inventive embodiments of the present inventionare described below.

In one embodiment, a method is presented for predicting lithium batteryproperties. The method includes an operation for creating an equivalentcircuit of a battery cell, where the equivalent circuit includes acathode equivalent circuit and a remainder equivalent circuit. Further,parameters for the cathode equivalent circuit are calculated usingQuantum Mechanical (QM) simulation. Also included in the method areoperations for obtaining parameters for the remainder equivalent circuitvia experimentation, and for calculating the lithium battery propertiesusing the equivalent circuit. In one embodiment, the remainderequivalent circuit includes an anode equivalent circuit, and anelectrolyte separator equivalent circuit.

In one embodiment, the anode equivalent circuit includes at least oneimpedance. In another embodiment, the electrolyte separator equivalentcircuit includes at least one capacitor and at least one resistor inparallel with the at least one capacitor. In yet another embodiment, thecathode equivalent circuit includes a voltage source that generates andopen circuit voltage (OCV) dependent on the lithium concentration x, anda bulk resistance as a function of the lithium concentration in serieswith the voltage source.

In one embodiment, calculating parameters for the cathode equivalentcircuit includes calculating OCV according to the formulaOCV(x)=−{G[Lix2 Host]−G[Lix1 Host]−(x2−x1)G[Li]}/(x2−x1), where G[Lix2Host] and G[Lix1 Host] are Gibbs free energies of the host electrodematerial at different lithium concentrations x1 and x2, x1 and x2 beinglithium concentrations samples, and G[Li] being the Gibbs free energy ofLithium. In another embodiment, calculating parameters for the cathodeequivalent circuit includes calculating the bulk resistance by executingion diffusivity or mobility transition barrier calculations.

In another embodiment, a method includes obtaining QM discharge curvesof the cathode based on the OCV and the bulk resistance from QMsimulated data, and obtaining the equivalent circuit parameters for therest of the circuit from experimental discharge curves via fabricationand measurement of coin or half cell discharge curves with standardanodes and electrolytes. In another embodiment, a method includesoperations for combining the QM discharge curve of a cathode with anexperimentally parameterized discharge curve for the rest of theequivalent circuit, which includes an anode and an electrolyte to form acombined discharge curve, and for displaying the combined dischargecurve as a total discharge curve of the coin cell or half cell made witha QM designed and parameterized cathode and an experimentallyparameterized anode and electrolyte. In one embodiment, a full celldischarge curve is obtained with QM designed electrodes as thedifference between a QM designed and parameterized cathode dischargecurve and a QM designed and parameterized anode discharge curve.

In another embodiment, an equivalent circuit for predicting lithiumbattery properties is presented. The equivalent circuit includes acathode equivalent circuit; an anode equivalent circuit; and anelectrolyte separator equivalent circuit. The electrolyte separatorequivalent circuit is connected serially between the cathode equivalentcircuit and the anode equivalent circuit, where the parameters for thecathode equivalent circuit are calculated using QM simulation. Further,the parameters for the anode equivalent circuit and the electrolyteseparator equivalent circuit are obtained via experimentation. Theproperties for the lithium battery are calculated using the equivalentcircuit.

In yet another embodiment, a computer program embedded in anon-transitory computer-readable storage medium, when executed by one ormore processors, is provided for predicting lithium battery properties.The computer program includes program instructions for creating anequivalent circuit of a battery cell, with the equivalent circuitincluding an anode equivalent circuit and a remainder equivalentcircuit. Further, the computer program includes program instructions forcalculating parameters for the anode equivalent circuit using QMsimulation, and for obtaining parameters for the remainder equivalentcircuit via experimentation. In addition, the computer program includesprogram instructions for calculating the lithium battery propertiesusing the equivalent circuit.

Other aspects of the invention will become apparent from the followingdetailed description, taken in conjunction with the accompanyingdrawings, illustrating by way of example the principles of theinvention.

BRIEF DESCRIPTION OF THE DRAWINGS

The invention may best be understood by reference to the followingdescription taken in conjunction with the accompanying drawings inwhich:

FIG. 1 illustrates at a high level the process for the fast design ofLi-ion batteries, according to one embodiment.

FIG. 2 is a high level flow chart of a method for testing and selectingLi-ion battery materials, structures, and compositions, in accordancewith one embodiment.

FIGS. 3A-3D present an embodiment of a method for screening andoptimizing battery materials for Li-ion batteries.

FIG. 3E illustrates a sample structure of the database holding batterymaterial information, according to one embodiment.

FIGS. 4A and 4B illustrate the crystalline structures of an ideal and acation disordered defected lattice structures, according to oneembodiment.

FIGS. 5A and 5B show the simulated XRD spectra generated by thedevelopment engine for the structures of FIGS. 4A and 4B, respectively,according to one embodiment.

FIG. 6A illustrates the hybrid model for a typical half cell setup thatconsists of a cathode, an electrolyte separator, and an anode, accordingto one embodiment.

FIG. 6B summarizes the impact of the parameters of the equivalentcircuit of FIG. 6A.

FIG. 6C illustrates the accuracy level of predicted battery propertiesbased on the amount of experimentation or simulation performed.

FIGS. 7A-7C illustrate the benchmarking of the hybrid model for a halfcell of LiCoO₂, according to one embodiment.

FIG. 8 shows a flow chart of a method used to calculate the simulatedcurves of FIGS. 7A-7C, in accordance with one embodiment.

FIGS. 9A and 9B present the Quantum Mechanical (QM) discharging curveusing the hybrid model as well as a comparison to a half cell data usingL333 as the cathode, according to one embodiment.

FIGS. 10A-10C illustrate an embodiment of a method for predicting theelectrochemical characteristics of full cells with new cathodematerials, even when real synthesis is not available, applying thehybrid model.

FIG. 11 illustrates one embodiment of a Graphical User Interface (GUI)of the development engine for searching battery materials.

FIG. 12A charts a comparison between predicted values and experimentalvalues for the differential voltage of different compositions.

FIG. 12B presents a comparison of the experimentation results and thesimulation results for the estimation of battery capacity.

FIG. 13 depicts an exemplary computer environment for implementingembodiments of the invention.

DETAILED DESCRIPTION

Embodiments of the invention provide methods, systems, and computerprograms for a fast and high-throughput design engine platform for theselection of quantum simulated Li-ion battery materials that conform torequirements of structure, safety, cycling ability, capacity, and powervariation. The determination of the materials is based on quantumsimulations where a database of modular elements for the simulations iskept for fast search and selection of the best structures for Li-ionbatteries. It will be obvious, however, to one skilled in the art, thatthe present invention may be practiced without some or all of thesespecific details. In other instances, well known process operations havenot been described in detail in order not to unnecessarily obscure thepresent invention.

In one embodiment, the system creates all possible compositionallydifferent structures of the layered oxide, spinel, and olivine-typeelectrode materials, as well as their solid solutions and mixed variantssuch as composite materials. In another embodiment, the platformprovides screening of all the created materials structures according totheir relative performance for providing better safety, longer cyclelife, higher nominal voltage, higher capacity, and higher rate or powerfor a Li-ion battery. The platform technology provides fast screeningfor safety, cycling ability, voltage, capacity, and rate or powercharacteristics of all the created structures from the quantum simulatedbuilding blocks in the database. Further, the platform providesincrementally higher accuracy and fine grain screening on a short listof candidate materials for safety, cycling, nominal voltage, capacity,and power.

A battery material-to-cell system level design and development engine,referred to herein as the development engine, is provided that allows auser to select inputs (e.g., composition for simulation), requestcomputations, generate capacity information, specify hierarchicalscreening criteria, etc. The development engine includes an easy-to-useGraphical User Interface (GUI) to accomplish these tasks. Further, thedevelopment engine enables the screening or filtering of a wide varietyof positive and negative electrode materials which are then used withgiven electrolyte materials for system level design of all cylindricaland prismatic Li-ion battery cells. The architecture and theimplementation of the quantum-simulation-driven material search anddesign platform allows quantum simulated atomic variation in theelectrode materials properties to be directly linked to the performanceof Li-ion battery cells for better safety, longer cycling ability,higher nominal voltage, higher capacity, etc.

FIG. 1 illustrates at a high level the process for the fast design ofLi-ion batteries, according to one embodiment. In operation 102, theproperties of simulated structures are calculated based on theproperties of quantum-simulated structures kept in a database and basedon the input materials class, the candidate materials, and thecompositional ratios of the elements chosen. A structural analysis 104of the simulated structures is performed via X-ray diffraction (XRD) orNeutron Diffraction (ND) software tools that obtain the simulated XRDand ND spectra of all the defected and non-defected structures.

Based on the most probable group of candidate structures from operation104, the method obtains the simulated capacity 106 for the selectedstructures by doing additional simulations of delithiation of thecandidates, unless the information on the delithiation candidatesalready exists in the database. Delithiation is the extraction of Liions from the lattice of the cathode material and insertion into thelattice of the anode of a Li ion battery. In operation 107 a hybridmodel approximation is used to calculate half cell discharge curves. Themodel used is called a hybrid model because it is capable of combiningdesigned electrode material quantum simulation data with experimentaldata for electrolyte and counter electrode effects.

In operation 108, the data for a simulated fuel cell is obtained.Operation 108 runs a system level battery cylindrical tool or aprismatic cell design tool, both of which are part of the developmentengine. The design engine gets as one of the inputs the simulated halfcell discharge curves calculated with the hybrid model in operation 107.After validating the results, one or more materials are selected fortesting in a Li-ion battery 110.

Generally, the speed of the simulations is inversely related to theaccuracy of the results, i.e., the longer the program runs performingthe simulations, the more accurate results the program will produce.Obviously, the more complex algorithms require longer running times.Different types of simulations and models have different levels ofcomplexity and running time, which result in differences in the accuracyof the results for the simulations. The linearized mixing, weightedmixing, and traditional composite based mixing methods (e.g.,Halprin-Tsai model extended to multi-component elemental systems) give avery fast approximation to the true solution and are used for coarsegrain searching and screening of the compositional and structuralvariations in a large range of structures and properties. Theintermediate range mixing methods are based on a mapping of thelocalized QS-DFT charges and energies from the modular building blocksto the larger structures. These intermediate range mixing methods areused for fine grain screening and searching in a short-listed range ofstructures identified with the faster methods. The final validation isobtained either via full QS-DFT simulations of the few selectedstructures or via synthesis performance evaluation of the chosencompositions and morphologies through experimentation. A validation byfull QS-DFT typically takes a few days to few weeks per model (amonghundreds to thousands of possible stoichiometric variations percomposition) depending upon how much previous data is available from thedatabase via the simulations, or few weeks per composition using fullexperimental synthesis and characterization methods.

FIG. 2 is a high level flow chart of a method for testing and selectingLi-ion battery materials, structures, and compositions, in accordancewith one embodiment. The battery development system includes a databaseof quantum-simulated structures and related properties. The structuresin the database are used as modular “Lego™-like” building blocks forbattery electrodes and electrolyte materials used in Li-ion batteries.Embodiments of the invention provide a set of physics-based design rulesand models for creating and screening solid-solutions and compositemodels of complex materials with the goal of achieving better safety,longer cycle life, higher nominal voltage, increased capacity, greaterpower, etc.

A computer program for battery development, referred to herein as thedevelopment engine, includes a GUI that enables the user to make changesin the quantum or atomistic levels of the new battery electrode andelectrolyte materials incorporated into system level cylindrical andprismatic cell design. Through the GUI the user selects the parametersrelated to the different possible simulations and combinations ofmaterials.

The database of modular building blocks is continuously updated andexpanded using QS-DFT, semi-empirical or empirical classical potentialbased methods. Further, the design rules and development models providethe relative characterization of safety, cycling-ability, volumechanges, nominal voltage, capacity, and discharge curves of complexcomposite and solid solution battery electrode materials againstbenchmark materials.

A method 202 for creating a quantum simulation database of modularbuilding blocks of materials and creating and screening structures oflarger scale complex materials is described in U.S. application Ser. No.12/334,170, filed Dec. 12, 2008, and owned by the assignee of thepresent application (the pending '170 application). More details ofmethod 202 are described below with reference to FIG. 3A.

Embodiments for determining the structure of a composite or solidsolution material for an electrode in a lithium-ion battery arepresented. More particularly, such materials are used in a cathode.Transition metal atoms that may be used for the composite or solidsolution materials include, but are not limited to, Sc, Ti, Zr, V, Nb,Cr, Mo, W, Mn, Fe, Co, Ni, Cu, Pd, Pt, Tc, Ru, Rh, Cd, Ag, Au, Y and Zn.

The methods described herein may also be used, for example, fordetermining the structure of an alloyed anode material in a lithium-ionbattery. In such methods for alloyed anode materials, an active backboneelement in the structure of the alloyed anode material, like thetransition metal atoms in the composite or solid solution material for acathode, are substituted. Active backbone elements for the alloyed anodematerial may include, but are not limited to, B, Al, Ga, C, Si, Ge, Sn,N, P, Sb, Bi, O, S, Se, Te, Zn, Cu, Ag and Au.

X-ray diffraction (XRD) yields the atomic structure of materials and isbased on the elastic scattering of X-rays from the electron clouds ofthe individual atoms in the system. In operation 204, the quantumsimulated relaxed and defected structures of battery materials aregenerated by the development engine. The coordinates of these structuresare used as inputs for an integrated XRD/ND tool within the developmentengine which returns the simulated XRD/ND spectra of QS simulatedmaterials structures. In one embodiment, the experimentalcharacterization of materials structures synthesized in the laboratory,which takes the spectrum of a synthesized material, is compared to theobserved peaks of known crystalline structures to characterize thestructure of the synthesized material. More details of operation 204 aredescribed below with reference to FIG. 3D.

In operation 206, a fast evaluation of material characteristics isperformed. The characteristics include safety, cycling ability,capacity, voltage, volume change on charge discharge, etc. More detailsof operation 206 are described below with reference to FIG. 3B.

Operation 208 involves building coin cells and validating the simulateddischarge curves using a hybrid half cell model. More details ofoperation 208 and the hybrid half cell model are given below withreference to FIGS. 3C and 6A-6B. Further, operation 210 includes runningthe development engine to design and test via the simulation of theelectrodes for cylindrical and prismatic full cells using the simulatedhalf cell discharge curves previously obtained. the development engineperforms the simulation of half cell discharge curves for the QSdesigned electrode active material and the testing of the designedelectrode with user specified parameters against standard or customizedcounter electrodes and electrolytes.

The obtained performance for the selected and designed structures ischecked in operation 212 to determine whether the performance meets therequirements for the materials. If the requirements are met, the methodcontinues to operation 214 where an actual coin cell is built and testedto validate the simulation results. If the requirements are not met, themethod returns to operation 202.

FIGS. 3A-3D present an embodiment of a method for screening andoptimizing battery materials for Li-ion batteries. As previouslydescribed, the pending '170 application describes in detail methods forcreating a database of quantum simulated building blocks and methods forscreening or filtering the chosen or designed candidate materialsstructures. The screened or filtered structures are those that have beenclassified such that structures in the same classification have the sameor similar properties. From all possible combinations of structuresderived from a specific query, the structures are ranked according to anenergy criteria, and the structures with the highest ranking forstability are selected for further analysis. The pending '170application presents methods and systems for determining the structureof a composite or solid solution material for an electrode of alithium-ion battery. In one method, a building-block database ofhypothetical structures containing only one transition metal atom isconstructed by use of quantum simulation. Then, a composite model set ofstructures containing two or more transition metal atoms is constructedby calculating a linear average of parent components from thebuilding-block database of hypothetical structures to determine latticeconstants and atomic coordinates of candidates. The composite model setis screened or classified into one of a plurality of possible subsetsusing a local order matrix such that composite models in the same subsetshare a property in local transition metal ordering. Further, arepresentative model from each subset is selected and a quantumsimulation on the representative model is performed to determine thestructure and properties of the material.

Referring now to FIG. 3A, in operation 102, the building block databaseis created. The building blocks are models, where each building blockmodel could be a real or a hypothetical structure containing one or moretransition metal atoms in their crystal unit cells. The simplicity ofthe model makes accurate QS search of new architectures possible in atimely manner. For example, replacing Co in layered (or spinel) LiCoO₂with another transition metal element forms a new constitutive crystalto be used later as a component of solid solution models. The buildingblocks may or may not be physically feasible or synthesized in thelaboratory, and yet could serve as the computationally derived buildingblocks to determine the search criteria and domain of more complex solidsolutions or composite materials that are feasible and that can besynthesized for lithium-ion battery applications.

The database of such modular building block materials structures and therelated properties includes QS-DFT simulated lattice constants, atomicconfigurations, relative energies, charge distributions, volume changes,and solubility for lithiated and delithiated, oxygenated and oxygenextracted, and cation disordered states of the same. In one embodiment,a complex solid-solution or composite material is broken up to generatea library of QS-DFT simulated modular building blocks such that many ofthe desired structural, safety, and electrochemical performancecharacteristics can be simulated on the fly using the physics basedhierarchical models and design rules described below.

FIG. 3E illustrates a sample organization of the database holdingbattery material information, according to one embodiment. Field 352defines the structure for which different types of data are kept, suchas the data defined by fields 368, 370, and 374, described in moredetail below. Structure 352 is defined by a formula and a structuretype, which is defined in field 354. The structure type 354 can besingle-crystal non-defected, single-crystal defected, composites(mixture of two or more single types), or a compositional formularepresenting the structure. The compositional formula is defined infield 356, which includes a list of different elements, such as Ni, Co,Mn, etc. Each element is included in the formula with a given percentageto form the compositional formula.

Structure type 354 is associated with a material class 364, whichincludes a list of defects in the structure. Examples of the materialclass include Lithium Cobalt Oxide (LCO), Lithium Nickel Manganese Oxide(LNMO), Lithium Iron Phosphate Oxide (LFPO), etc. The different types ofdefects are defined in field 366, and include delithiated (L),deoxygenated (O), cation disorders (C), mobility barriers (M), vacancies(V), surfaces (S), grain boundaries (G), interfaces (I), etc. Part 360defines whether the structure is being used as a cathode, an anode, oran electrolyte. Further, field 358 defines the lattice for the cathode,such as layered, spinel, olivine, or composite.

Field 370 defines whether the data type corresponds to raw data fromsimulation or the data is experimental data for comparison. In otherembodiments, other types of data are also kept in the database, such astest data, experimental data, etc. Some simulation data is kept inrecords associated with field 368, which includes spectra obtainedthrough XRD or ND simulations, test and validation data, energies of thestructures, mobility, etc. Field 374 includes values for one or moreproperties of the structure, such as safety, cycling, voltage, capacity,differential voltage, volume change, discharge curve, etc.

Field 372 defines the algorithm used for the simulation, that is, thehalf cell discharge curve model such as the hybrid model describedherein, Nelson model, the FreedomCAR model, etc. Each of the models maystore some of the calculations or parameters obtained during thesimulation. For example, field 376 keeps the values obtained when usingthe hybrid model. The hybrid-model values include Open Circuit VoltageOCV(x), R_(bulk)(X), C_(int), R_(int), Z_(others), experimentalparameters, etc.

It should be noted that some of the fields or records described abovemay be empty for some structures, as not all data is required orobtained at the same time. For example, the test/validation data is onlycalculated when requested by the user or by a computer program. Itshould be also noted that the embodiment illustrated in FIG. 3E isexemplary. Other embodiments of the database may utilize differentarrangement of the data or different fields. The embodiment illustratedin FIG. 3E should therefore not be interpreted to be exclusive orlimiting, but rather exemplary or illustrative.

Returning to FIG. 3A, in operation 104 user inputs are captured. In oneembodiment, the inputs include the material class or type, thecomposition, and the formula, but other inputs, such as morphology,particle size, etc., are also possible. The inputs can be obtained usingthe GUI described below with reference to FIG. 11. Next in operation106, the method selects suitable building blocks from the database andcombines the selected blocks to create all possible models of complexstructures. Additionally, the system generates the relative totalenergies for all the possible models of complex structures.

In operation 108, the models of the structures are grouped by thecorresponding relative total energies in order to screen for stability.The method constructs a composite model set of derivative or daughterstructures containing two or more transition metal atoms by calculatinga linear average of parent components from the building block databaseof hypothetical structures to determine the lattice constants and atomiccoordinates of candidate composition models. The structures obtainedthis way are found to be nearby a total energy minimum.

Next, in operation 110 the method screens or classifies the compositemodel set by employing a local order matrix to sub-classify eachcomposite model into a subset or group such that the composite models ineach subset or group share the similar property in local transitionmetal ordering. A representative model from each subset or group is thenselected according to its stability. The selected candidates from eachsubset or group are ranked in terms of the relative total energies orthe highest stability criteria. The most likely candidates are chosenaccording to their rank, i.e., according to their lowest total energy orhighest stability criteria.

FIG. 3D describes a method for performing structural analysis of thecandidate materials. FIGS. 4A-4B and 5A-5B, described in more detailbelow, present structures and results obtained during the structuralanalysis. The data related to experimentally obtained materials is keptin the database. However, the actual composition of these experimentallyobtained materials is not known. One embodiment of the invention is usedto compare the data obtained through simulation with the data fromexperimentally obtained materials. Once a match is found, the methodthen determines the composition of the experimentally obtained materialsas that of the corresponding simulated structures with the same spectra.The structural analysis is based on XRD of quantum simulated andscreened structures according to their stability, as previouslydescribed with reference to operations 108 and 110 to quantify thestructurally defected and modified materials structures.

In operation 401, the spectra of an experimentally synthesized materialis obtained and then stored in the database. In operation 402 thedefected structures are selected based on the properties to be analyzed(e.g., oxygen removal, cation disorder, vacancies, surfaces, etc.) Inone embodiment, the same structures selected in operation 110 of FIG. 3Aare chosen. In other embodiments, a subset of these defected structuresis chosen. Any ratio, fractional amount, and compositional mixtures ofthe cation disorder, vacancy creation, surfaces, oxygen removal typepoint defects as well as phase and grain boundaries type crystalstructure defects can be calculated in the simulated materialsstructures.

The user can select a type of defect (e.g. oxygen removal) using the GUIin the development engine, and then the user or the development enginecreates different defected structures for that type of defect bychanging the amount of defect introduced (10%, 15%, 20%, etc.). Forexample, the crystalline structures of the ideal

is shown in FIG. 4A, and the crystalline structures of the cationdisordered defected

is shown in FIG. 4B, where 11% of the Li is exchanged with Ni in

. The transition metal atoms layer (third row from the bottom in FIG.4B) shows the exchange of Li with the transition metal atoms 452 in thelayer.

As previously discussed, the quantum simulated relaxed and defectedstructures of battery materials are generated with the developmentengine. The coordinates of these structures are used as inputs for theintegrated XRD/ND simulation tool which returns in operation 404 thesimulated XRD/ND spectra of QS simulated pristine and defected materialsstructures. The resulting spectra for the pristine and the defectedstructures are described in more detail below with reference to FIGS. 5Aand 5B. The results of the XRD and ND simulations are added to thedevelopment engine database in operation 406.

The suitable geometry and the suitable stoichiometry compositions of theideal and defected materials structures are obtained in order to designthe new battery materials, as well as quantifying the defects in thegenerated materials. In one example, the simulation produces a defectedstructure of the cation disorder by exchanging the coordinates of onepair of the Ni—Li atoms in the structure, and then producing the XRDstructure.

The results from experimentally synthesized materials are also includedin the database. These synthesized materials are created in the lab bychanging the synthesis conditions, such as temperature, duration of theexperiment, impurities, etc. However, the composition of theseexperimentally synthesized materials is not exactly known due to thechanges in the environmental conditions.

Returning to FIG. 3D, in operation 408 the simulated XRD patterns of thedefected structures are compared to the XRD patterns of theexperimentally synthesized materials. In one embodiment, the coordinatesof the peaks in the spectra of the simulated structures are comparedwith the coordinates of the peaks from the experimentally synthesizedmaterials. It should be noted that a certain margin of differences maybe within normal tolerance, and a match may be determined when thespectra are substantially similar. In operation 410, the results of thecomparison in operation 408 are used to determine whether the methodflows to connector D (i.e., back to the beginning to restart theprocess) when no match is made, or flows to operation 412 when a matchis made. In operation 412, the amount of the defects in theexperimentally synthesized materials is then determined as the defectsin the corresponding simulated structure. This allows the user of thedevelopment engine to identify and characterize defects in the defectedcompositions of the materials synthesized in experiments.

FIGS. 5A and 5B show the simulated XRD spectra generated by thedevelopment engine for the structures of FIGS. 4A and 4B, respectively,according to one embodiment. The comparison of the position and strengthof the extra peaks in the XRD spectra of the defected structures in FIG.5A with that of the pristine structures in FIG. 5B is used tocharacterize and quantify the defects in the experimentally synthesizedmaterials. This is just one example of how to characterize cationdefects in the experimentally synthesized materials structures using thesimulated XRD spectra of the development engine. All other type ofdefects, such as those listed in field 366 of FIG. 3E, can also besimilarly characterized by the simulated spectra created by thedevelopment engine and by comparing with the experimentally synthesizedmaterials under different synthesis conditions.

Returning to FIG. 3B, in operation 202 the user selects which analysisto perform next, either a structural analysis or a battery propertyanalysis. If the structural analysis is chosen, the method flows tooperation 402 in FIG. 3D to perform the structural analysis, aspreviously described. If the user selects the battery property analysis,the method flows to operation 204, as described above in operation 110of FIG. 3A, where the most likely group of candidate structures isselected by the screening procedure. The method employed for batteryproperty analysis is referred to herein as the battery Capacity andVoltage Prediction using Quantum simulations (CVPQ) method, whichincludes operations 204, 206, 208, and 210 from FIG. 3B.

In operation 206, the development engine determines which candidates aremissing in the database of simulated structures and need a simulation.In operation 208, new simulations are performed for the candidates, ifany, that need a simulation, such as additional simulations for newbuilding block structures. The results of the additional new simulationsare the delithiated structures and the energies of these delithiatedstructures. After operation 208, the method flows to operation 210 torun the fast material level analysis and obtain the value of thedifferent parameters, such as voltage, volume change oncharging/discharging, capacity, relative safety, relative cycling, etc.

The first operation in the fast material level analysis includesperforming standard Quantum Mechanical (QM) total energy calculations atdifferent delithiated structures. A sample calculation for Li_(x) CoO₂(LCO) is included below for illustrating purposes, such that the CVPQmethod calculates standard QM total energy calculations at differentdelithiated structures for the variable x in Li_(x) CoO₂. Delithiatedstructures of Li_(x) CoO₂ are derived structures from a fully lithiatedLCO structure. However, the symmetry of Li_(x) CoO₂ is not necessarilythe same as that of fully lithiated LCO. In one embodiment, delithiatedstructures are constructed from fully lithiated LCO that can be made byusing modeling methods, such as the one illustrated in FIG. 3A. Forexample, a minimum of three or more sampling points of lithiumconcentration are selected for evaluating the electrochemicalcharacteristics, such as working voltage and capacity.

The QM total energy calculations can be performed by all availablefirst-principle approaches, such as DFT-based methods, all of itsvariants, and all of its equivalents known by different names, as wellall the semi-empirical methods where some parts of the total energyfunction are approximated and some parts are simulated. The averaging ofthe simulated electrochemical characteristics, such as working voltageand capacity along the charge or discharge curves, is typically doneover many simulated values of these characteristics, where eachsimulated value uses a minimum of three sampling points for differentvalues of the variable x (delithiation.) The selection of a minimum ofthree sampling points for the value of x is exemplary and otherembodiments of the method can use a different number of sampling pointsfor different lithium concentrations. The larger the number of samplingpoints used in the procedure, the more accurate and reliable the finallypredicted results will be.

The calculation of the average voltage for two lithium concentrations isperformed using the following formula known in the art:

$\begin{matrix}{{V(x)} = \frac{- \left\{ {{E\left\lbrack {{Li}_{x_{2}}\mspace{14mu}{Host}} \right\rbrack} - {E\left\lbrack {{Li}_{x_{1}}\mspace{14mu}{Host}} \right\rbrack} - {\left. 〚{\left( x〛 \right._{2} - x_{1}} \right){E\lbrack{Li}\rbrack}}} \right\}}{\left. 〚{\left( x〛 \right._{2} - x_{1}} \right)}} & (1)\end{matrix}$

In equation (1), E represents the total energy of the composite or solidsolution and x₁ and x₂ are the lithium concentration sampling of thecomposites. It is preferable that the total energies used in equation(1) be calculated by the same QM method to avoid any inconsistency amongdifferent implementations of QM. Additionally, it is preferable to usethe same approximation for all energy functional terms to avoid anyinconsistency among different energy functional approximations. Forexample, one DFT package may implement several Generalized GradientApproximations (GGA) versions, such as GGA+U or screened exchange (SX).In this case, if data from different implementations of the DFT ondifferent parent building blocks has to be used, then proper scalingmethods are used to bring the data to a same relative reference valuebefore using the data in the above procedure. It is also possible tocombine data obtained from different methods using proper scalingprocedures, although the thus obtained results will typically be lessaccurate.

The fast evaluation method approximates the electrochemicalcharacteristics of a candidate electrode as a cathode or as an anode inLi-ion Batteries (LIB) as a fitting function of lithium concentration(x), also referred to as a functional form of (x). Initially V(x) iscalculated according to the following formula:V(x)=V _(oc) +C ₁(−1)  (2)

In equation (2), the coefficients V_(oc) and C₁ are fitting parametersderived from average voltages obtained from applying equation (1) usingthe total energies of the delithiated structures at different samplingpoints. The calculated values for LCO are presented in Table A below.Often, QM underestimates the voltage as compared to experimentallyobtained voltage values. Therefore, in one embodiment, a phenomenaladditional reference value correction is added to the parameter V_(oc)depending on which property is to be corrected. This adjusted value ofV_(oc) is referred to as shifted V_(oc). In another embodiment, theadditional reference value correction for the same electrochemicalproperty is kept the same for all the building blocks and simulatedstructures among the same family of the materials type. This way therelative values of the simulated electrochemical properties within thesame material class or type are not affected. For example, an additionalreference value correction of 0.6V can be used for the simulatedcapacity and 1.5V for the simulated nominal voltage in all LCO andlayered-oxide type electrode materials irrespective of single ormultiple transition elements used in the formulation. For differentmaterials structure types, such as spinel or olivine, the additionalreference value corrections are different and need to be accounted forwhen comparing the simulated values across different materials type.

The linear functional form in equation (2) is just one example of alinear functional form. Other formulas are also possible. For example,the linear case is one instance of a more generic fitting curve with thefollowing definition:V(x)=V _(oc) +C ₁(x−1)+D(x−1)² +E(x−1)³  (3)

As in equation (2), in equation (3) V_(oc) is related to voltage and C₁is a parameter related to a capacity value. Further, D and E areparameters accounting for higher derivatives of the capacity.

Capacity is a function of the lithium concentration for a given workingvoltage window. The coefficients V_(oc) and C₁ are determined by solvingthe fitting function (i.e., equation (2)) for two different values of x,as described above. The capacity of the material depends on the value ofx at which V(x) in equation (2) is equal to the cut-off voltageV_(cut-off) for the cell. For example, the capacity of an electrode withcut-off voltage at 4.3V is different and less than the capacity of anelectrode with cut-off at 4.6V. Which cut-off voltage is used (e.g.,4.3V or 4.6V) depends on the application under consideration. Therefore,once the cut-off voltage is fixed from the application view point,fitting function (2) is solved to find the x at which V(x)=V_(cut-off).Once the value of x corresponding to the V_(cut-off) is known, thecapacity is calculated from the maximum capacity Q_(mx) of the material.The capacity is equal to xQ_(mx). The theoretical maximum capacity forany material is calculated by the chemical formula of the material. ForLCO, Q_(mx) is 274 mAh/g. Table A below, which is a summary of theresults obtained using equation (2) shows that the QM capacity of LCO is175 mAh/g at 4.3V cut-off. This value is similar to the chargingcapacity of 174 mAh/g and the discharging capacity of 171 mAh/g at 0.2 Cat cut-off 4.3V for coin cells data. This approach for the fastestimation of the capacity from the voltage profile emphasizes the lowrate flat linear region of the voltage profile and assumes that thecontribution at the edges near the lower and upper cut-off voltages areminimal and can be ignored for fast relative comparisons.

The nominal voltage of a cell is the average voltage over thedischarging period, and is a function of the voltage cut-off. Thenominal voltage in experiments is generally determined by the flatlinear region of the voltage profile as a function of the state ofcharge. In the fast evaluation method, the nominal voltage is defined asan average between the V_(cut) and the shifted V_(oc), where V_(cut) isthe cut-off voltage as fixed by the application under consideration. Theaccuracy of the nominal voltage thus obtained can be iterativelyincreased by using more sampled data points for different lithiumconcentrations on the voltage profile, and by using an average value ofthe shifted V_(oc) instead of the single value of the shifted V_(oc)determined by only two lithium concentration data points. Furtheriterations using more sampled data-points of lithium concentrationsalong the voltage profile increase the accuracy of the predicted nominalvoltage by the fast estimation method. For LCO, a QM nominal voltage of4.1V is predicted, which is similar to the plateau between 3.9 V and 4.2V observed in half cells using LCO as the cathode.

Table A below summarizes the results of applying the method for thesample Li concentrations of ½, ⅔, and ¾.

TABLE A QM electrochemical calculations of LCO Li Concentration × ½ ⅔ ¾QM total energy (au) −1547.7627 −1549.0363 −1549.6723 Average voltage(V) (½, ⅔) 3.252 Average voltage (V) (⅔, ¾) 3.000 Fitting coefficientsV_(oc) = 2.412 (V), C₁ = −2.016 Phenomenal corrections Capacity shift =0.6 V, Nominal voltage shift = 1.5 V QM capacity 175 mAh/g at 4.3 V vs.Exp charge/discharge capacity of 174/171 mAh/g QM nominal voltage 4.1 Vvs. Exp plateau range: 3.9-4.2 V

For composites that can be constructed using building blocks, the sameCVPQ method illustrated above for the LCO example can be used to performa fast evaluation of the electrochemical characteristics by treating thecomposite as a combined building block. For example, in the case ofcomposite Li(Ni_(1/3)Co_(1/3)Mn_(1/3))O₂ (L333) the QM total energycalculations can be performed on three sampling points at differentlithium concentrations and then follow the CVPQ method described aboveto derive the electrochemical characteristics.

Another embodiment for a method to perform fast evaluation ofelectrochemical characteristics of composite structures is describedbelow. To illustrate the method, composite L333 is evaluated usingindividual building blocks' electrochemical characteristics previouslyobtained using the CVPQ method.

Table B below shows the electrochemical characteristics of individualbuilding blocks Lithium-nickel oxide (LNO), LCO, and Lithium ManganeseOxide (LMO), which were obtained performing the CVPQ method illustratedfor LCO.

TABLE B QM electrochemical CVPQ calculations of L333 from buildingblocks Materials QM capacity Exp. Charging/discharging (cut-off at 4.3V) (mAh/g) Capacity (mAh/g) LNO 213 ~219 LCO 175 174/171 (0.2 C) LMO 210Unknown L333 (bare) 202 200/180 (1 C)   L333 (weighted) 197

A first strategy, referred to herein as strategy A, approximates theelectrochemical properties of the composite structure using aHalpin-Tsai combination of the electrochemical properties of individualbuilding blocks. As an illustrating example, the capacity of L333 is aspecial case of the following general formula:Q(Lxyz)=f[x,y,z;Q _(LNO) ,Q _(LCO) ,Q _(LMO)]  (4)

In equation (4), the parameter f is a Halpin-Tsai type function withvariables x, y, and z for the component ratio of each building block ina general composite Lxyz. In the case of L333, x, y, and z are all equalto ⅓. The fifth row of Table B shows the QM capacity of L333 to be 202mAh/g by using the Halpin-Tsai type combination, as is known in the art.

A second strategy, referred to herein as strategy B, adopts a weightedHalpin-Tsai type combination according to the prospected different rolesof individual building blocks in the composite phase. In strategy B,weighted Halpin-Tsai variables, such as x*W_(x) are used instead of thebare Halpin-Tsai variables of strategy A. For example, it is assumedthat LNO is the main capacity contributor because the valence of Ni iongoes from 2+ to 4+ during the discharging period. Other terms can beignored. The sixth row of Table B shows the QM capacity of L333 to be197 mAh/g when using the weighted Halpin-Tsai type combination (strategyB).

Both QM capacities obtained using strategies A and B are similar to theactual charging capacity of about 200 mAh/g and the discharging capacityat 180 mAh/g at 1 C. Columns 2 and 3 of Table B present the availablesimulation data and the experimental values. By comparing the valuesfrom columns 2 and 3, it can be observed that the fast methodcalculations obtained with the present method are similar for bothindividual building blocks and for composites.

Continuing with reference to FIG. 3B, after operation 210, the methodflows to operation 214 where a check is performed to determine whetherany of the designed materials meet the basic requirements for thebattery. If the result of the check is negative, then the method flowsback to operation 104 in FIG. 3A. Otherwise, if the result of the checkis positive, the method flows to operation 216 where a subset of thecandidate materials is selected for complex analysis included in thesimulation of half cell discharge curves. In another embodiment, all thematerials that meet the requirements are selected. After operation 216,the method flows to operation 302 of FIG. 3C.

With reference to FIG. 3C, operation 302 checks whether the Li ionmobility or diffusion data is present in the database for the candidatebeing analyzed. If the mobility or diffusion data is in the database,then the method proceeds to operation 306. Otherwise, the methodproceeds to operation 304 where the Li ion mobility in many delithiatedstructures is calculated. The final results of the additionalcalculations include the OCV and the resistance of the delithiatedstructures using the mobility or diffusion data. Once the Li ionmobility is calculated, the new results are added to the database.

In operation 306, a hybrid half cell model is used to obtain the halfcell discharge curves. The hybrid model is described below withreference to FIG. 6A. In operation 308, coin cells are built to validatethe simulated discharge curve of operation 306.

From operation 308, the method flows to operation 312 to determinewhether there is any cell that meets the performance and safetyrequirements. If no cell meets the requirements, then the method returnsto operation 104 to re-start the process. However, if one or more cellsmeet the requirements, then the method continues to operation 310 wherecylindrical and prismatic full cells are designed with simulated halfcell discharge curves. The thus designed and optimized prismatic andcylindrical full cells are then fabricated in operation 314 and testedin operation 316 for performance, safety, and cycling to validate thesimulation results and choose the designed candidate material.

FIG. 6A illustrates the hybrid model for a typical half cell setup thatconsists of a cathode, an electrolyte separator, and an anode, accordingto one embodiment. The model is referred to as a hybrid model because itcombines simulation data and experimental data. The data for the cathodeor the quantum designed electrode is obtained using QM simulations andthe data for the anode and the electrolyte is obtained via a fewbenchmark experiments for a given class of materials. The cellequivalent circuit is divided into a cathode equivalent circuit and aremainder equivalent circuit, which includes the electrolyte separatorequivalent circuit and the anode equivalent circuit.

In other embodiments, the same methodology described herein is used forthe anode and the electrolyte and the use of the hybrid model is notrequired. This means that the data for the anode and the electrolytes iscalculated using simulations and stored in the database for use with thealgorithms described herein to obtain data for the use of the differentmaterials in building battery cells.

In accordance with the hybrid model, the electrolyte separator, which issoaked with appropriate electrolyte, allows Li ions to shuttle betweentwo electrodes while electrically isolating the two electrodes. In oneembodiment of a half cell, the anode is a Li metal. The electrochemicalcharacteristics of a half cell are mainly determined by theelectrochemical properties of the cathode or designed materials. Thehybrid model includes, (1) creating an equivalent circuit of the cell,and (2) determining the values of the components in the equivalentcircuit.

The circuit components of FIG. 6A are grouped into three distinct groupsaccording to their relations to the lithium concentration x in thecathode. The first group is the Open Circuit Voltage OCV(x) and bulkresistor R_(bulk)(x). Both OCV(x) and R_(bulk) are highly dependent onthe lithium concentration of the cathode. The second group is a pair ofcomponents connected in parallel, an interface capacitor and aninterface resistor, C_(int) and R_(int). This pair of componentsaddresses the electrical contribution by the cathode and the electrolyteinterface. A simple approximation to the cathode-electrolyte interfaceincludes the parameters C_(int) and R_(int) used to represent a weakdependence on the lithium concentration of the cathode.

The third group corresponds to the Li metal anode and is parameterizedinto a single impendence Z_(others). It is assumed that Z_(others) isindependent of the lithium concentration of the cathode. Therefore,Z_(others) contributes universal electrical impedance to theelectrochemical characteristics of a half cell. In one embodiment, thepolarization effects on the metal-electrolyte interface are consideredinsignificant and a real resistor R_(others) is used instead of thecomplex Z_(others).

The hybrid model presented in FIG. 6A is one example of a circuitrepresentation for the different components of a battery. Otherembodiments of the invention may use other combinations of elements. Forexample, in one embodiment, the electrolyte separator includes more thanone resistor connected in series or in parallel, and one or morecapacitors connected in series or in parallel with any combination ofthe resistors for the equivalent circuit of the electrolyte separator.Similarly, the anode can be represented by several impedances connectedin series, in parallel or in a combination of series and parallelconnections, where each impedance can be a resistor or a capacitor.

In another embodiment, the anode parameters are obtained thoroughsimulation (as previously discussed for the cathode), and the cathodeparameters are obtained through experimentation. Moreover, anycombination of simulated data and experimental data for cathode, anode,and electrolyte can be used in different embodiments of the invention.

The accuracy of the hybrid model depends on how each circuit componentis parameterized. In one embodiment, the parameterization combinespartial experimental fitting with QM determination for certaincomponents in order to retain a high degree of prediction power to LIBmaterials and system designs. The more QM determination is used for theindividual circuit components, the more powerful the prediction andimprovement of LIB materials and system designs. In one embodiment, QMcalculations are performed to determine the bulk properties of thecathode, and then other components are fit for the properties of thebenchmark half cell data for a given class of materials.

FIG. 6B summarizes the impact of the parameters of the equivalentcircuit of FIG. 6A. In regard to the relationship to the cathode, therelationship to the cathode by the OCV(x) and R_(bulk)(x) are theparameters in bulk material, the parameters and R_(int) are related tothe interface material, and Q_(others) is not related to the cathode.Regarding the effect of the Li concentration x, OCV(x) and R_(bulk)(x)have a strong relationship to the Li concentration in cathode, andR_(int) have a moderate dependence on the Li concentration in cathode,while Z_(others) is not dependent on the Li concentration in cathode.

FIG. 6C illustrates the accuracy level of predicted battery propertiesbased on the amount of experimentation or simulations performed. Aspreviously discussed, the accuracy of the results is related to theamount of simulations performed, but the accuracy is also related to thefact whether the data is collected via QM simulations or from actualexperimentation. The least amount of accuracy corresponds to the dataobtained only through simulation, while the most accurate data on thedischarge curve is obviously obtained by experimentation, becauseaccuracy is a measure of the difference between the simulated andexperimentally measured discharge curves. In the middle of these twoextreme approaches, the hybrid model combines QM simulation data withexperimental data on a few benchmark materials in a given class toobtain the simulated discharge curves, which are faster to obtain andare accurate enough to filter or screen many candidate structures tomake a short list before synthesizing the needed materials performingthe actual electro-chemical testing.

FIGS. 7A-7C illustrate the benchmarking of the hybrid model for a halfcell of LiCoO₂, according to one embodiment. FIG. 7A illustrates the QMcalculated OCV(x) for an LCO cathode at 0.2 C and for different Liconcentrations. FIG. 7B illustrates the QM calculated R_(bulk)(x) forthe different Li concentrations. Further, FIG. 7C shows the fitteddischarge curve and a comparison with experimental coin cell data. FIG.7C shows that the fitted discharge curve is almost the same as thedischarge curve measured through experimentation.

FIG. 8 shows a flow chart of a method used to calculate the simulatedcurves of FIGS. 7A-7C, in accordance with one embodiment. In operation802, the method performs a standard QM calculation of OCV(x) using thefollowing formula:OCV(x)=−{G[Li_(x2)Host]−G[Li_(x1)Host]−(x ₂ −x ₁)G[Li]}/(x ₂ −x ₁)  (5)

In equation (5), G is the Gibbs free energy as a function of thedelithiated structure [Lix Host], where x₁, x₂ are concentrations of thedelithiated host lattice in the application range of interest of thecomposites. G[Li] corresponds to the Gibbs free energy of individualLithiums. The more sample points and the more accurate QM, then the moreaccurate the OCV(x) will be.

In operation 804, a standard QM calculation of R_(bulk)(x) is performedby executing ion diffusivity or mobility transition barrier calculationsas is known in the art. See, for example, A Van der Ven, G. Ceder,Journal of Power Sources 97-98, (2001) 529. Further, in operation 806the method combines the OCV(x) from operation 802 and the R_(bulk)(x)from operation 804 to obtain the bulk QM discharging curve using theequivalent circuit model of FIG. 6A.

Standard coin cells are fabricated during operation 808 by using a LCOcathode in a half cell setup. Discharging measurements at 0.2 C or atother rates are then performed. In operation 810, the method averagesthe previously obtained discharging curves over at least 10-20 coin celldata points to get a reproducible and reliable experimental dischargingcurve.

In operation 812, the method fits the QM discharging curve to anexperimentally parameterized discharging curve using the equivalentcircuit model illustrated in FIG. 6A, including the anode and theelectrolyte. The development engine displays the combined dischargecurve as the total discharge curve of the coin cell or half cell madewith the QM designed and parameterized cathode and the experimentallyparameterized anode and electrolyte. As can be observed in FIG. 7C, theQM curve obtained approaches the experimental discharging curve fairlywell. In one embodiment, the QM and experimental discharging curves ofFIGS. 7A-7C are displayed by the development engine on a display duringoperation 814.

Another application of the hybrid model is the prediction of theelectrochemical characteristics of new cathode materials, even when realsynthesis and discharge curve data on the new material is not available.This is achieved by simulating QM prediction of the relativeelectrochemical discharge characteristics with respect to the benchmarkmaterial such as LCO for single-crystalline layer oxides. An example ispresented below to illustrate this method for L333 (i.e.,Li(Ni_(1/3)Co_(1/3)Mn_(1/3))O₂) type materials. The following operationsare performed:

1. Perform a standard QM calculation of OCV(x) for L333 using the sameQM method and the same lithium concentration sampling mesh (x), andcalculate dOCV(x) as the OCV difference between L333 and LCO point bypoint, i.e., dOCV(x)=OCV_(L333)(x)−OCV_(LCO)(x). As previouslydiscussed, the more Li concentration points are sampled, the morereliable the QM calculation procedure will be.

2. Replace OCV_(LCO)(x) with OCV_(L333)(x), and perform the hybridmethod illustrated in FIG. 8 for LCO to get a QM discharging curve forL333 at low rates.

3. Perform standard QM calculation of R_(bulk)(x) for L333 using thesame QM method and the same lithium concentration sampling mesh (x), andcalculate R_(bulk) difference dR_(bulk)(x) between L333 and LCO point bypoint, dR_(bulk)(x)=R_(bulk:L333)(x)−R_(bulk:LCO)(x). The more samplesare calculated, the more reliable the QM calculations will be.

4a. Use R_(bulk)(x) for L333 to replace R_(bulk)(x) for LCO, and thenperform the CVPQ method to get a QM discharging curve for L333 at lowrates.

4b. In another embodiment, the method uses both OCV_(L33)(x) from andR_(bulk)(x) for L333 to replace the same term for LCO and then performthe CVPQ method to get a QM discharging curve for L333 at low rates.

4c. In another embodiment, the previously obtained OCV difference,dOCV(x), is added to the LCO coin cell discharging curve according tothe equivalent circuit model of FIG. 6A. FIGS. 9A and 9B present the QMdischarge curve using the hybrid model as well as a comparison to a halfcell data using L333 as the cathode, according to one embodiment. The QMdischarging curve fairly approximates the experimental coin cell data.

4d. In another embodiment, the calculated R_(bulk) difference,dR_(bulk)(x), is added to the LCO coin cell discharging curve accordingto the equivalent circuit model and then follow the method of operation4c to derive a new QM discharging curve.

4e. Another embodiment uses both dOCV(x) and dR_(bulk)(x) and adds themto the LCO coin cell discharging curve according to the equivalentcircuit model.

In general, the more QM calculations of OCV, R_(bulk), and theirdifferences with respect to LCO are performed, the more accurate andpowerful the prediction of the discharging curves will be.

FIGS. 10A-10C are graphs that illustrate an embodiment of a method forpredicting the electrochemical characteristics of full cells with thenewly QM simulated or designed cathode materials, even when realsynthesis is not available, by using the simulated discharge curves andthe above-described hybrid half cell model. Full cells can beconstructed from two half cells that have different voltage-capacitycharacteristics. The method is illustrated by constructing the dischargecurve of a typical 18650 battery, which uses LCO as the cathode andgraphite as the anode. In one embodiment, the same QM discharge curve ofFIG. 10A is used from the example of LCO for cathode previouslydescribed with reference to FIGS. 7A-7C. In addition, the coin celldischarging curve of a graphite as the anode is also used, as shown inFIG. 10B. The full cell discharging curve is a combination of the twodischarging curves according to the following equation:Vfull cell(x)=Vcathode(x)−Vgraphite(x)  (6)

In another embodiment, the simulated half cell discharge curve data ofthe designed or developed cathode, using the hybrid model describedabove, is passed as an active cathode material input discharge curve toany full cylindrical or prismatic cell design, testing, and validationtool such as Battery Design Studio (BDS), which is a commerciallyavailable tool from Battery Design LLC, or any other such tool. The BDSuses the QM simulated discharge curve of the cathode, under the hybridmodel, as the input active cathode material discharge curve. BDS allowschoosing all the cathode side slurry parameters, such as particle size,surface area, Li concentration, binder type and concentration, andconducting agent type and concentration. BDS allows the design of thefull cylindrical or prismatic cell positive electrode or cathode with QMsimulated discharge curve using the hybrid half cell model. In anotherembodiment, BDS similarly allows choosing the anode and electrolyte froma database of standard anodes and electrolytes used in industry andacademia.

In another embodiment, the QM designed and developed cathode or positiveelectrode material, using simulated half cell discharge curves with thehybrid model, can be combined with standard anodes or electrolytesavailable from the BDS database to design cylindrical or prismatic fullcell batteries and simulate their electrochemical discharge and safetycharacteristics.

In yet another embodiment, the QM designed and developed cathode orpositive electrode material, using simulated half cell discharge curveswith the hybrid model, can be combined with customized anodes orelectrolytes, for which data is available from any other source, or datathat can be generated in experiments, to design cylindrical or prismaticfull cell batteries to simulate their electrochemical discharge andsafety characteristics.

In another embodiment, it is possible to test and validate the designedor developed positive electrode or cathode against standard orcustomized anodes or electrolytes. They are tested and validated forperformance and safety characteristics at the system level for fullcylindrical or prismatic cell configurations. The test and validationare performed on a computer to screen or short list the candidatematerials before any materials synthesis is performed, and a full cellis designed and developed for the synthesized material.

The accuracy of the designed, tested and validated material at thesystem level full cylindrical or prismatic cells will depend on theamount of QM simulated positive electrode or cathode material datatogether with amount and accuracy of experimentally measured anode,electrolyte, or interface related data.

In another embodiment, it is possible to extend this methodology isextended to use QM simulated or new anode and electrolyte data withstandard, designed or developed new cathode material data as well.

FIG. 10C shows an example of a discharge curve at 1 A current for atypical 18650 full cylindrical cell battery, which yields a capacity of2.2 Ah, fairly matching the actual capacity of existing 18650 batteries.Similar discharge curves with typical prismatic cells are also feasiblewith the development engine methodology.

FIG. 11 illustrates one embodiment of a Graphical User Interface (GUI)of the development engine for searching battery materials. The GUI setsup an interaction mechanism between a user and the computer program,including database data and logic flow, for the candidate electrodematerial's screening-optimization procedures. The search for materialsincludes the goals of obtaining better safety, cycling ability, nominalvoltage, higher capacity, and increased power. It allows the selectionof electrode materials and combinations of selected electrolytematerials for system level cylindrical or prismatic cell design.

The development engine is based on the database of QS-DFT simulatedmodular building block structures and implements one or more of thepreviously described physics-based hierarchical models. Further, thedevelopment engine implements the design and screening rules to searchfor new battery materials compositions enabling the user tointeractively manage and organize the process flow to perform thefollowing tasks:

(a) Receive user input to select the single, composite, or solidsolution lattice types, mole or composition ratio of active elements,and end functional group to determine the composition to be screened;

(b) Create a set of all possible models of the target composition fromthe database of modular building blocks;

(c) Structurally screen the set of generated models to separate themodels into groups that need to be simulated for the targetedstructural, safety, and performance characteristics;

(d) Display the structural models and their X-ray diffraction spectrafor comparison or validation with experimentally synthesizedcompositions;

(e) Simulate and display the relative safety, cycling ability, nominalvoltage, capacity and volume change on charging/dischargingcharacteristics of the selected composition to screen the structures bycomparing them with a chosen benchmark or according to the user requiredcriteria;

(f) Simulate and display the electrochemical discharge characteristicsof the chosen or selected composition, using the hybrid model, incomparison with the discharge characteristics of the benchmark materialscomposition within the chosen class of material; and

(g) The simulated discharge characteristics results obtained for thechosen or screened composition are combined with the user supplied inputon morphology, surface area, and tap density to design cylindrical orprismatic electrodes and cells with the required safety and performancecharacteristics.

The development engine allows designers to rapidly eliminatenon-performing compositions and focus their efforts on the promisingcandidates. The design process is guided by the development engine andcan be broken into four phases that can be iterated until desiredresults are achieved. These four phases are:

Phase 1: Material Composition & Structural Analysis;

Phase 2: Material Intrinsic Electrochemical Properties;

Phase 3: Link to Coin Cell or Half Cell System Discharge Curves; and

Phase 4: System-level cylindrical or prismatic cell design, test,validation, and comparison performance.

It should be noted that the embodiments using four phases are exemplary.Other embodiments may utilize different number of phases and theoperations in each phase may be different. The embodiments illustratedshould therefore not be interpreted to be exclusive or limiting, butrather exemplary or illustrative.

In the embodiment shown in FIG. 11, the top half is dedicated for inputsand the bottom half includes buttons that perform calculations orpresent information on the display. After the user selects the inputs,such as the material composition, then the user selects whichinformation is of interest. This way, the user gets information fasteras the development engine does not need to compute all the possibleitems of information. If information is requested and is not available,the development engine calculates it on demand and informs the user thatadditional data is needed in the database to complete the desired task.

In phase 1, the elements and the composition are chosen. Radio buttons192 allow the selection of the type of battery material: cathode, anode,or electrolyte. Additionally, the type of lattice can also be selectedusing radio buttons 194, including Layered, Spinel, Olivine, etc.Additionally, the number of elements, the elements, and the fractionalcomposition for each element is selected in input area 152. For example,in the selection shown in FIG. 11, the formula LiNi_(x) Co_(y)Mn_(z)O₂has been selected for 3 elements: Ni, Co, and Mn. The parameters x, y, zcan be between 0 and 1 with x+y+z=1 (100%), and in the example shownx=0.6, y=0.2, and z=0.2, which means a composition of 60% Ni, and 20%each of Co and Mn.

When the user clicks button 154, the atomic scale models areconstructed. For any chosen composition hundreds to thousands of atomicscale models are possible where Ni, Co, or Mn have distinct positionassignments. The Construction button 154 causes the development engineto develop all possible models for structural and energy analysis forstability.

Screen structures button 156 is used to perform screening in the orderof stability. For the chosen composition, all the generated models arescreened and ordered in terms of relative energies and separated intogroups, such that groups with lower energies are more feasible andstructurally stable. Display and structural analysis button 158 causesthe development engine to display, for the members of the selectedgroups, the analysis of atomic arrangements, bond, lengths, bond angles,etc.

Cation disorder button 160 is used for creating defects. Cation disorderdefects in the created structures are responsible for performancedegradation, which can be quantified with the use of XRD spectralanalysis. The listing of cation disorder defect in button 160 is used asone example of the capability to examine and analyze different types ofdefects possible in the material. Other embodiments may utilize othertypes of defects such as oxygen removal or vacancy, vacancy creation,grain-boundaries, interfaces or surface defects. The option provided bybutton 160 should therefore not be interpreted to be exclusive orlimiting, but rather exemplary or illustrative. The development enginecreates the chosen percentage of defects, such as the cation disordersrelated to the cycling ability of the material. Clicking XRD button 162starts the XRD/ND Analysis. The development engine allows fast andinstantaneous analysis of X-ray and Neutron Diffraction spectra of thechosen composition and structures of the pristine and defected material.The resulting spectra are available for display. Both simulations can becompared with experimental data to characterize the experimentallysynthesized material.

Phase 2 is categorized under the Performance section, and includesbuttons 164, 166, 168, 170, and 172. Safety button 164 is selected todetermine the relative oxygen release rate (ORR) in relation to safety.The intrinsic relative safety property of the chosen material isassessed by the relative ease with which oxygen is released by thematerial. The ORR is the transition rate computed by QM simulations ofthe activation energy of oxygen removal. The ORR is a pre-factor, whichis determined by the ratio between the partition function at thetransition location and the partition function of the initialconfiguration. When calculating the relative safety property of thebattery, the relative ORRs are computed as a ratio with respect to theORR of the benchmark material. Initially, for fast estimation, it can beassumed that the changes in the pre-factors are small with respect tothe benchmark material as compared to the changes in the exponentfactors arising out of the activation energies. However, ultimately asthe database is populated over time with different transition states andwith the corresponding pre-factors, the effect of pre-factors in theabsolute ORRs could be included instead of the relative ORRs. The ORR,which can be shown on the display, is used in screening the chosencomposition for safety. The larger the ORR, the less safe the chosencomposition will be.

Cycling button 166 is labeled “Cycling” to calculate and display theintrinsic relative cycling ability at the material level by comparingthe relative cation disorder formation rate. The intrinsic relativecycling property of the chosen material is computed by calculating therelative ease with which a Ni—Li, Co—Li, or Mn—Li exchange cationdisorder is formed in the layered oxides and the formation of suchdefects is shown to reduce the intrinsic cycling ability at thematerials level. A relative cation disorder formation rate (CDFR) isused in screening the chosen composition for cycling ability. The CDFRis a transition rate computed by QM simulations of the activation energyof Ni—Li, Co—Li, or Mn—Li exchange and a pre-factor determined by theratios of the partition function at the transition location to thepartition function of the initial configuration before exchange. Therelative CDFRs are computed as a ratio in respect to the CDFR of thebenchmark material. For fast estimation, it can be assumed that thechanges in the pre-factors are small with respect to the benchmarkmaterial when compared to the changes in the exponent factor arising outof the activation of exchange energies. However, as the database ispopulated with different transition states and the pre-factorscorresponding to those transition states, the effect of pre-factors inthe absolute CDFRs can be included instead of the relative CDFRs. Thelarger the CDFR, the poorer the cycling ability of the chosencomposition will be.

Button 168, labeled “Vol. Change,” calculates and displays the volumechange on charging and discharging. The charging and discharging of abattery cathode material involves removal and restoration of lithiumions. The difference between the volume of the initially relaxedstructures and the volume of the same delithiated structures is thevolume change computed using the QM methods. Further, the volume changeof the material is computed as the percentage volume change as afunction of the composition.

Button 170 calculates and displays the differential voltage. The rate oftotal energy change is a function of lithiation and delithiation andindicates the differential voltage of the material. The computation ofthe differential voltage is described above with reference to equation(1) as an example using LCO. The same procedure can be applied to othermaterials as well. The differential voltage, which varies according tothe composition, is correlated with the nominal voltage and can be usedto screen the chosen composition for a given nominal voltage. In oneembodiment, the computation of the nominal voltage is described abovewith reference to Table A for the case of LCO. The same method can beused for other materials as well.

The last button in phase 2 is button 172, labeled “capacity”, whichdetermines and displays the specific capacity of the battery. The rateof total energy change as a function of lithiation and delithiation andthe limit up to which the battery electrode material is stable upondelithiation, as determined by the simulations, is used to compute theintrinsic specific capacity (e.g., in mAh/g) of the material withingiven upper and lower cutoff voltages. In one embodiment, an uppercut-off voltage of 4.2V is used for capacity computations. In otherembodiments, different upper cut-off voltages are possible to use inbutton 172 of phase 2. One embodiment for the fast estimation of thecapacity is described above with reference to equation (2) for the caseof LCO. The same method can be applied to other materials as well.

Phase 3 includes the selection of the hybrid model and computation ofcoin cell discharge rate behavior. Button 174 selects model 1, thehybrid half cell model described hereinabove. As discussed above, it ispossible to use DFT quantum simulated data for the designed cathodeactive material with standard electrolyte and anode materials at thecoin cell level to determine the discharge rate of the cell. If desired,additional models (e.g., models 2 and 3) can also be provided. In oneembodiment, model 2 is the Nelson model and model 3 is the Freedom CARmodel.

Buttons 176 and 178 use the hybrid model to calculate the coin celldischarge rate behavior. The QS DFT simulated delithiated structures inphase 2 are used for simulating mobility or resistance of Li iondiffusion as a function of delithiation. This information is combinedwith the experimental resistance or mobility for the anode and theelectrolyte to compute the low (e.g., 0.2 C) and high (e.g., 10 C)discharge rate behavior of the chosen material. Button 176 calculatesthe QM V(x) low and button 178 calculates the QM V(x) high.

Phase 4 is under the “Cylindrical” label and includes operations 180,182, 184, 186, and 188.

Cell button 180 opens the Battery Design Studio (BDS) simulation tool.The Battery Design Studio (BDS) is a system level cell design softwaretool, which is commercially available from Battery Design, LLC ofYokohama Japan. BDS is just one example of the full cell system leveldesign software and tools developed over years by universities, industryand government labs. Across the board, the BDS and other full cellsystem level design tools and software are based on the experimentallyobtained discharge curves of the electrode materials. The software toolsuse experimentally obtained discharge curves of the given electrodematerial with a counter electrode and an electrolyte to design andsimulate the performance of cylindrical or prismatic full cells. In oneembodiment, the simulated half cell discharge curves of QM designedelectrode materials are used with a given counter electrode andelectrolyte, as described above with reference to the hybrid model andFIGS. 6A-6C. The results are fed as input to the BDS, or some othersystem level full cell design and evaluation tool. The use of the hybridmodel together with software tools, such as BDS, allows the design,testing and evaluation of system level cylindrical or prismatic fullcells with QM designed electrode material in a given counter electrode,electrolyte, separator, and balance of materials (BOM) for full cells.Button 182 calculates the design for the cylindrical full cells with BDSusing the QM designed and simulated cathode material. The low rate(e.g., 0.2 C) discharge behavior of the chosen active materialcomposition is used with standard binder, conductivity aid, electrolyte,and anode materials to design 18650 cylindrical cells with computedsystem level capacity and discharge characteristics.

Button 184 performs the testing of the cylindrical full cells designedin option 182. The charging and discharging behavior of the designedcell under user-defined procedures is tested by running the user-definedprocedures. The procedures are generally specific to and explained inthe BDS or other specific system level cylindrical or prismatic fullcell design and evaluation tool or software. The results are displayedto the user.

Button 186 performs comparisons of the cylindrical cells. The charge anddischarge behavior of the designed cell, with the chosen cathodematerial composition, is compared to the charging and dischargingbehavior of the similar size cell and other cathode material chemistriesas described in the user-manual of BDS, or some other system leveldesign tool, used for buttons 180-186. The results are presented on thedisplay. Buttons listed under 190 are the same buttons under cylindricalbatteries, except that they are applied to prismatic batteries.

FIG. 12A charts a comparison between predicted values and experimentalvalues for the differential voltage of different compositions. Althoughthe values are fairly close, the values obtained with the developmentengine were slightly (5-10%) smaller than the actual values obtainedthrough experimentation. FIG. 12B presents a comparison for theestimation of battery capacity. In this case, the development enginepredicted slightly higher values than those obtained throughexperimentation.

FIG. 13 depicts an exemplary computer environment for implementingembodiments of the invention. It should be appreciated that the methodsdescribed herein may be performed with a digital processing system, suchas a conventional, general-purpose computer system. Special purposecomputers, which are designed or programmed to perform only onefunction, may be used in the alternative. The computer system includes acentral processing unit (CPU) 1304, which is coupled through bus 1310 torandom access memory (RAM) 1306, read-only memory (ROM) 1312, and massstorage device 1314. Development engine program 1308 resides in randomaccess memory (RAM) 1306, but can also reside in mass storage 1314.

Mass storage device 1314 represents a persistent data storage devicesuch as a floppy disc drive or a fixed disc drive, which may be local orremote. Network interface 1330 provides connections via network 1332,allowing communications with other devices. It should be appreciatedthat CPU 1304 may be embodied in a general-purpose processor, a specialpurpose processor, or a specially programmed logic device. Input/Output(I/O) interface provides communication with different peripherals and isconnected with CPU 1304, RAM 1306, ROM 1312, and mass storage device1314, through bus 1310. Sample peripherals include display 1318,keyboard 1322, cursor control 1324, removable media device 1334, etc.

Display 1318 is configured to display the user interfaces describedherein, such as the GUI shown in FIG. 11. Keyboard 1322, cursor control1324, removable media device 1334, and other peripherals are coupled toI/O interface 1320 in order to communicate information in commandselections to CPU 1304. It should be appreciated that data to and fromexternal devices may be communicated through I/O interface 1320. Theinvention can also be practiced in distributed computing environmentswhere tasks are performed by remote processing devices that are linkedthrough a wire-based or wireless network.

Embodiments of the present invention may be practiced with variouscomputer system configurations including hand-held devices,microprocessor systems, microprocessor-based or programmable consumerelectronics, minicomputers, mainframe computers and the like. Theinvention can also be practiced in distributed computing environmentswhere tasks are performed by remote processing devices that are linkedthrough a network.

With the above embodiments in mind, it should be understood that theinvention can employ various computer-implemented operations involvingdata stored in computer systems. These operations are those requiringphysical manipulation of physical quantities. Any of the operationsdescribed herein that form part of the invention are useful machineoperations. The invention also relates to a device or an apparatus forperforming these operations. The apparatus may be specially constructedfor the required purpose, such as a special purpose computer. Whendefined as a special purpose computer, the computer can also performother processing, program execution or routines that are not part of thespecial purpose, while still being capable of operating for the specialpurpose. Alternatively, the operations may be processed by a generalpurpose computer selectively activated or configured by one or morecomputer programs stored in the computer memory, cache, or obtained overa network. When data is obtained over a network the data may beprocessed by other computers on the network, e.g., a cloud of computingresources.

One or more embodiments of the present invention can also be fabricatedas computer readable code on a computer readable medium. The computerreadable medium is any data storage device that can store data, whichcan be thereafter be read by a computer system. Examples of the computerreadable medium include hard drives, network attached storage (NAS),read-only memory, random-access memory, CD-ROMs, CD-Rs, CD-RWs, magnetictapes and other optical and non-optical data storage devices. Thecomputer readable medium can include computer readable tangible mediumdistributed over a network-coupled computer system so that the computerreadable code is stored and executed in a distributed fashion.

Although the method operations were described in a specific order, itshould be understood that other housekeeping operations may be performedin between operations, or operations may be adjusted so that they occurat slightly different times, or may be distributed in a system whichallows the occurrence of the processing operations at various intervalsassociated with the processing, as long as the processing of the overlayoperations are performed in the desired way.

Although the foregoing invention has been described in some detail forpurposes of clarity of understanding, it will be apparent that certainchanges and modifications can be practiced within the scope of theappended claims. Accordingly, the present embodiments are to beconsidered as illustrative and not restrictive, and the invention is notto be limited to the details given herein, but may be modified withinthe scope and equivalents of the appended claims.

The invention claimed is:
 1. A computerized method for fabricating alithium battery including designing the lithium battery, the methodcomprising: providing a quantum simulation database comprising buildingblocks of models of materials for use in designing the lithium battery,wherein the building blocks of models of materials comprise real andhypothetical structures containing one or more transition metal atoms intheir crystal unit cells; inputting, by a user, input informationrelated to at least one material used to design the lithium battery viaa user interface; generating at least one candidate structure from thebuilding blocks in the database based on the input information; andobtaining simulated half cell discharge curves of the at least onecandidate structure using a hybrid model, the hybrid model comprising anequivalent circuit of a battery cell for the at least one candidatestructure, the equivalent circuit including a cathode equivalent circuitand a remainder equivalent circuit, wherein the cathode equivalentcircuit includes a voltage source that generates an open circuit voltage(OCV) dependent on a lithium concentration x, and a bulk resistance as afunction of the lithium concentration in series with the voltage source,and wherein data for the cathode equivalent circuit including the OCVand bulk resistance is obtained from Quantum Mechanical (QM) simulation,and data for the remainder equivalent circuit is obtained fromexperimentation, fabricating coin cells based on the at least onecandidate structure; testing the fabricated coin cell for performance,safety and cycling and validating the simulated half cell dischargecurves with coin cell discharge curves obtained from the fabricated coincells; and fabricating full cells after the simulated half celldischarge curves are tested and validated.
 2. The method as recited inclaim 1, wherein the bulk resistance is obtained by executing iondiffusivity or mobility transition barrier calculations.
 3. The methodas recited in claim 1 comprising: obtaining the simulated half celldischarge curves based on the OCV and the bulk resistance from QMsimulated data; and wherein the data for the remainder equivalentcircuit is obtained from experimental discharge curves of coin cellswhich are fabricated with standard anodes and electrolytes.
 4. Themethod as recited in claim 3, further including: combining the simulatedhalf cell discharge curves with the experimental discharge curves toform a combined discharge curve; and displaying the combined dischargecurve as a total discharge curve.
 5. The method as recited in claim 4,further including obtaining a full cell discharge curve of a full cellwith QM designed electrodes as a difference of a QM designed andparameterized cathode discharge curve and a QM designed andparameterized anode discharge curve.
 6. The method of claim 1 whereinthe building blocks are models of structures of one or more transitionalmetal atoms in crystal unit cells.
 7. The method of claim 1 wherein thedatabase includes material structures and related properties of thebuilding blocks.
 8. The method of claim 7 wherein the related propertiesof the building blocks comprise QS-DFT simulated lattice constants,atomic configurations, relative energies, charge distributions, volumechanges, and solubility for lithiated and delithiated, oxygenated andoxygen extracted and cation disorder states or a combination thereof. 9.The method of claim 1 wherein the data for the cathode equivalentcircuit is obtained from calculating OCV according to a formula:OCV(x)=−{G[Li_(x2) Host]−G[Li_(x1) Host]−(x ₂ −x ₁)G[Li]}/(x ₂ −x ₁),where x₁ and x₂ are lithium concentrations, G[Li_(x1) Host] andG[Li_(x2) Host] are Gibbs free energies of a host electrode material atlithium concentrations x₁ and x₂, and G[Li] is a Gibbs free energy ofLithium.
 10. The method of claim 1 further comprises testing andvalidating the full cells.
 11. The method claim 10 comprises fabricatingthe lithium battery according to the full cells after being validated.